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EP3856835A1 - Mélanges élastomériques-polymères réticulés - Google Patents

Mélanges élastomériques-polymères réticulés

Info

Publication number
EP3856835A1
EP3856835A1 EP19783761.0A EP19783761A EP3856835A1 EP 3856835 A1 EP3856835 A1 EP 3856835A1 EP 19783761 A EP19783761 A EP 19783761A EP 3856835 A1 EP3856835 A1 EP 3856835A1
Authority
EP
European Patent Office
Prior art keywords
pipe
composition
polymer
elastomer
crosslinking
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP19783761.0A
Other languages
German (de)
English (en)
Inventor
Krishnan ANANTHA NARAYANA IYER
Antonios K. Doufas
Krassimir I. Doynov
Anthony J. Dias
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ExxonMobil Chemical Patents Inc
Original Assignee
ExxonMobil Chemical Patents Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ExxonMobil Chemical Patents Inc filed Critical ExxonMobil Chemical Patents Inc
Publication of EP3856835A1 publication Critical patent/EP3856835A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04—Homopolymers or copolymers of ethene
    • C08L23/06—Polyethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B1/00—Layered products having a non-planar shape
    • B32B1/08—Tubular products
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B15/00—Layered products comprising a layer of metal
    • B32B15/04—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B15/06—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of natural rubber or synthetic rubber
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B15/00—Layered products comprising a layer of metal
    • B32B15/18—Layered products comprising a layer of metal comprising iron or steel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B25/00—Layered products comprising a layer of natural or synthetic rubber
    • B32B25/14—Layered products comprising a layer of natural or synthetic rubber comprising synthetic rubber copolymers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
    • F16L11/00—Hoses, i.e. flexible pipes
    • F16L11/04—Hoses, i.e. flexible pipes made of rubber or flexible plastics
    • F16L11/10—Hoses, i.e. flexible pipes made of rubber or flexible plastics with reinforcements not embedded in the wall
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00—Properties of the layers or laminate
    • B32B2307/50—Properties of the layers or laminate having particular mechanical properties
    • B32B2307/558—Impact strength, toughness
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2597/00—Tubular articles, e.g. hoses, pipes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00—Applications
    • C08L2203/18—Applications used for pipes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
    • Y10T428/1386—Natural or synthetic rubber or rubber-like compound containing
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
    • Y10T428/139—Open-ended, self-supporting conduit, cylinder, or tube-type article
    • Y10T428/1393—Multilayer [continuous layer]

Definitions

  • Flexible pipes are used to transport fluids between oil and gas reservoirs and platforms for separation of oil, gas and water components.
  • the flexible pipe structures include layers of materials, the layers being, for example, polymeric, metallic, and composite layers.
  • conventional flexible pipes include an inner pressure sheath (a polymeric sheath) which contacts the fluids being transported in the flexible pipe. Because the inner pressure sheath contacts the fluids being transported in the pipe, good resistance to physical and chemical degradation, resistance to hydrolysis, and low permeability to various gases in the fluids transported is needed.
  • Offshore pipes generally comprise one or more tube-formed barrier layers including an inner liner and at least one reinforcing layer.
  • the inner liner is the innermost polymer layer, which in known offshore pipes also constitutes a barrier layer or a pressure sheath, and which is exposed to a fluid, e.g. oil transported in the pipeline.
  • the pipeline also comprises an outer sheath providing a barrier to the outer environment such as seawater.
  • the pipe normally comprises one or more reinforcing layers between the inner liner and the outer sheath, and some pipes also comprise a reinforcing layer inside the pipe, called a carcass. The carcass prevents collapse of the inner liner and provides mechanical protection to the inner liner.
  • Some pipes also comprise one or more intermediate polymer layers.
  • polyamides are susceptible to hydrolysis and aliphatic polyketones are also susceptible to degradation at elevated temperatures.
  • the permeability of gases increases with temperature, and polyethylene has a relatively high permeability and solubility to gases, which promotes blistering of the polyethylene material.
  • the interest in the industry for use of inner pressure sheath in corrosive applications with high concentrations of carbon dioxide and/or hydrogen sulphides is increasing.
  • permeation of gases like methane, carbon dioxide and hydrogen sulphide may in some cases be prohibitive for use of the polyethylene inner liners at high temperatures.
  • Other explored solutions to overcome these drawbacks, such as PVDF and Polyimides/Polyamides are substantially cost prohibitive.
  • EP 487 691 describes an inner pressure sheath of crosslinked polyethylene to overcome some of the disadvantages of conventional polyethylene.
  • An inner liner with such crosslinked material has shown to be improved compared to inner liners of the similar non- crosslinked (thermoplastic) material.
  • the process of producing an inner liner is carried out in two steps: first the material in non-crosslinked form is manufactured by extrusion, and afterwards the material is crosslinked.
  • a crosslinking step involves a pipeline that is first manufactured by extrusion of the inner layer of polyethylene, followed by metal armoring and outer sheathing. By this process, it is necessary to manufacture the entire pipe before making the actual crosslinking of the inner liner.
  • thermoplastic elastomers have found limited application in flexible pipe inner sheath.
  • TPEs are usually based on polymers which simultaneously have a) high crystallinity greater than 20 % and /or amorphous phase whose glass transition temperature is below room temperature, and b) an elastomeric phase that imparts substantially improved ductility.
  • the elastomeric phase and/or the amorphous region of the thermoplastic polymer can be crosslinked either via chemical or physical crosslinking.
  • FIG. 2 is an exploded perspective view of an unbonded flexible pipe, according to at least one embodiment.
  • flexible pipe means a flexible pipe or umbilical hose, or a flexible pipe combining the functions of flexible pipes and umbilicals, and can be used in off-shore/subsea or on-shore applications.
  • a percent tensile elongation at break (23°C) when exposed to aqueous solution of 18% calcium chloride and 14% calcium bromide at 90 °C for 4 weeks of about 200% or greater, such as about 150% or greater, such as about 100% or greater,
  • the polymer layer is passed from the extruder to the crosslinking zone with less than 25°C average intermediate cooling, such as less than lO°C average intermediate cooling, such as substantially no intermediate cooling.
  • average cooling means average temperature decrease through the thickness of the polymer layer.
  • the surface of the polymer layer may be cooled down more than the middle of the material.
  • the cooling of the surface of the polymer layer does not exceed 40°C, such as the cooling of the surface of the polymer layer does not exceed 20°C from the extruding zone to the crosslinking zone.
  • a crystalline polymer has a crystallinity of about 20% or greater and is selected from one or more of a polyethylene, a polypropylene, a silane-grafted polyethylene, a polyester, a nylon, a fluorothermoplastic polymer, and a poly ketone.
  • a crystalline polymer has a crystallinity of about 40% or greater and is selected from one or more of a polypropylene, a polyester, a fluorothermoplastic polymer, and a polyketone.
  • a crystalline polymer has a crystallinity of about 40% or greater and is a polyethylene.
  • a crystalline polymer has a crystallinity of about 40% or greater and is a polypropylene
  • a polyethylene resin having a multimodal molecular weight distribution can have (a) a density in the range from 0.925 g/ccm to 0.965 g/ccm, and (b) a melt index (12) from 0.1 g/lO min to 5 g/lO min, and (c) comprise a high molecular weight (HMW) component and a low molecular weight (LMW) component, and wherein the HMW component comprises at least one high molecular weight ethylene interpolymer having a density in the range from 0.910 g/ccm to 0.935 g/ccm, and a melt index of 1.0 g/lO min or lower, and wherein the LMW component comprises at least one low molecular weight ethylene polymer having a density in the range from 0.945 g/ccm to 0.965 g/ccm, and a melt index in the range from 2.0 g/lO min to less than 200 g/lO min, and wherein the at
  • the polyethylene includes a low density, linear low density, or high density polyethylene.
  • the polyethylene can be a high melt strength (HMS) long chain branched (LCB) homopolymer polyethylene
  • Crystallinity can also be determined by X-ray diffraction.
  • the fluorothermoplastic can have a softening or melting point that is from about 80°C to about 350°C.
  • a fluorothermoplastic for use herein can have a Tg that is in the range of about -l20°C to about +20°C, and typically about -95°C to about -20° C.
  • the blends of this disclosure can be processed and reprocessed by conventional plastic processing techniques such as extrusion, injection molding, blow molding, and compression molding.
  • An ethylene-derived content that is from about 10 wt% to about 99.9 wt%, (such as from about 10 wt% to about 90 wt%, such as from 12 wt% to about 90 wt%, such as from about 15 wt% to about 90 wt% such as from about 20 wt% to about 80 wt%, such as from about 40 wt% to about 70 wt%, such as from about 50 wt% to about 70 wt%, such as from about 55 wt% to about 65 wt%, such as from about 60 wt% and about 65 wt%) based on the total weight of the ethylene-propylene rubber.
  • the ethylene-derived content is from about 40 wt% to about 85 wt%, such as from about 40 wt% to about 85 wt%, based on the total weight of the ethylene-propylene rubber.
  • Elastomeric terpolymers are commercially available under the trade names VistalonTM (ExxonMobil Chemical Co.; Houston, Tex.), KeltanTM (Arlanxeo Performance Elastomers; Orange, TX.), NordelTM IP (Dow), NORDEL MGTM (Dow), RoyaleneTM (Lion Elastomers), and SupreneTM (SK Global Chemical). Specific examples include Vistalon 3666, Keltan 5469 Q, Keltan 4969 Q, Keltan 5469 C, and Keltan 4869 C, Royalene 694, Royalene 677, Suprene 512F, Nordel 6555.
  • Suitable nitrile rubbers according to the present disclosure can have a medium to high acrylonitrile content (ACN) for an acceptable degree of fluid and fuel resistance.
  • ACN medium to high acrylonitrile content
  • the nitrile rubbers according to the present disclosure can have an acrylonitrile content greater than 15 %, more preferably greater than 30 %, even more preferably greater than 39 % and most preferably, greater than 43 %.
  • Nitrile rubbers can have a Mooney viscosy to DIN 53 523 ML 1+4 at l00°C of from 3 to 150, such as from 30 to 130, such as from 40 to 120 Mooney units.
  • the Mooney viscosity (MLi +8 @l25° C.) of useful butyl rubber can be from about 25 to about 75, or from about 30 to about 60, or from about 40 to about 55.
  • the CSM can be a terminal silicone group(s), such as is found in silicone-crosslinking-group-terminated perfluoroalkylpolyethers, e.g., Shin-Etsu Sifel. Silicone CSMs are further described below in the discussion of CSMs.
  • the olefin When a repeating unit derived from an olefin is chosen, the olefin preferably has from 2 to 6 carbon atoms.
  • a typical curable rubber may include an ethylene, propylene or butylene repeating unit, the molar ratio of such olefin units to acrylate repeating units typically being less than 2, preferably being in the range from 0.5 to 1.5.
  • curable rubbers having a vinyl chloroacetate group are AR-71 and AR-72LS, available from Zeon Chemical Division of Nippon Zeon, and Europrene® R, L and S from Enichem; a representative curable rubber having a benzylic chloride group is Hytemp® 4051 also available from Zeon Chemical.
  • the functional groups that react to form the compatibilizer are at the terminus of the polymers.
  • a block copolymer comprising at least one segment each of nitrile rubber and an olefin polymer, said copolymer being derived from an olefin polymer containing one or more graft forming functional groups and a nitrile rubber containing one or more graft forming functional groups.
  • decomposition causes a crossbnking agent to release radical-formers which induce crossbnking in the TPE or TPV blend.
  • the crossbnking process could place in the continuous thermoplastic phase, the elastomer phase (if partially crossbnked in the TPE or TPV composition before entering the extruder) or both the thermoplastic and elastomer phases.
  • the temperature during the extrusion is typically between l45°C to 230 °C.
  • the temperature during extrusion is selected to keep the TPE or TPV blend in a molten state.
  • the crossbnking agent can have an activation temperature which is substantially above such as at least l°C, such as at least 5 to lO°C, above the temperature of the TPE or TPV blend during the extrusion.
  • the extruded TPE or TPV blend is subjected to a heat treatment in the crosslinking zone at a temperature above l45°C, such as at a temperature from l50°C and 250°C to activate the crosslinking agent.
  • the permeation barrier layer is essentially impermeable to sulphides at a partial pressure of 0.03 bars or more, such as 0.1 bars or more, and to methane at a partial pressure of 1 bar or more, such as 10 bars.
  • the flexible unbonded offshore pipe may have any shape e.g. as known from WO 00/36324 and U.S. Pat. No. 6,085,799, which are hereby incorporated by reference.
  • One or more of the tube-formed polymer layers, e.g. the inner liner, intermediate layer or layers and/or outer cover, may be produced using the process of the present disclosure.
  • the layer comprising a crosslinked TPV or TPE is at least one of the layers (usually a polymeric sheath) of the flexible pipe.
  • the flexible submarine pipe may comprise other layers in addition to those mentioned above.
  • the pipe may comprise: a collar carried by the short-pitch winding of at least one cross-sectional wire around the pressure vault to increase the resistance to the pipe bursting, and / or retaining layer such as a high strength aramid strip (Technora® or Kevlare) between the outer polymeric sheath and the tensile armor plies, or between two tensile armor plies, and / or and optionally an anti-wear layer of polymeric material such as plasticized polyamide.
  • aramid strip Technora® or Kevlare
  • FIG. 2 is an exploded perspective view of an unbonded flexible pipe 200 according to some embodiments.
  • the unbonded flexible pipe comprises from inside out a steel carcass 5, an inner sheath 4, pressure armor layers 3 and 3’, an anti wear layer 6, tensile armor layer 2a, insulation layer 7 (an intermediate sheath), tensile armor layer 2b, and an outer sheath 1.
  • Inner sheath 4 and steel carcass 5 contact the oil and/or gas during use.
  • the inner sheath 4 and/or outer sheath 1 are made from or comprise one or more layers, the one or more layers including a material comprising one or more crosslinked TPE or TPV blends.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Rigid Pipes And Flexible Pipes (AREA)

Abstract

Des modes de réalisation de la présente invention concernent généralement des compositions de TPE ou TPV réticulés, des tuyaux souples contenant des compositions de TPE ou de TPV réticulés, et des procédés de formation de compositions de polymère élastomère réticulé et de tuyaux souples ; dans un mode de réalisation, un tuyau flexible comprend une pluralité de couches, au moins une couche comprenant une composition comprenant : au moins un élastomère polaire, et un polymère ayant une cristallinité d'environ 20 % ou plus. Dans un mode de réalisation, un tuyau comprend une gaine interne, une gaine externe, une première couche de blindage et une seconde couche de blindage, au moins l'une de la gaine interne et de la gaine externe comprenant une composition de TPE ou TPV réticulés qui est le produit de réaction d'un élastomère ayant une polarité d'environ 90° ou moins, un polymère ayant une cristallinité d'environ 20 % ou plus, et un agent de réticulation.
EP19783761.0A 2018-09-24 2019-09-10 Mélanges élastomériques-polymères réticulés Withdrawn EP3856835A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201862735563P 2018-09-24 2018-09-24
PCT/US2019/050303 WO2020068409A1 (fr) 2018-09-24 2019-09-10 Mélanges élastomériques-polymères réticulés

Publications (1)

Publication Number Publication Date
EP3856835A1 true EP3856835A1 (fr) 2021-08-04

Family

ID=68165702

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19783761.0A Withdrawn EP3856835A1 (fr) 2018-09-24 2019-09-10 Mélanges élastomériques-polymères réticulés

Country Status (4)

Country Link
US (1) US20210340361A1 (fr)
EP (1) EP3856835A1 (fr)
CN (1) CN113166499A (fr)
WO (1) WO2020068409A1 (fr)

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JP7411892B2 (ja) * 2019-04-24 2024-01-12 住友理工ホーステックス株式会社 高圧ホースおよびその製造方法
CN113411737B (zh) * 2020-03-17 2023-03-10 3M创新有限公司 用于微型扬声器的音膜及其制备方法
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